MX2014001324A

MX2014001324A - Additives for ceramic glazes.

Info

Publication number: MX2014001324A
Application number: MX2014001324A
Authority: MX
Inventors: Giovanni Floridi; Stefano Crespi; Bassi Giuseppe Li; Dario Chiavacci; Mattia Canziani; Laura Vigano'
Original assignee: Lamberti Spa
Priority date: 2011-08-01
Filing date: 2012-07-20
Publication date: 2014-02-27
Also published as: US9399601B2; ITVA20110023A1; RU2603683C2; US20140165875A1; EP2739579B1; PL2739579T3; RU2014107912A; BR112014001420A2; CN103717545A; WO2013017445A1; CN103717545B; ES2561889T3; EP2739579A1

Abstract

Use of extruded pellets comprising carboxymethyl cellulose and at least another ceramic glaze additive for the preparation of ceramic glaze slips.

Description

ADDITIVES FOR CERAMIC ENAMELS FIELD OF THE INVENTION The present invention relates to the use for the preparation of ceramic enamel slips of extruded pellets comprising a carboxymethyl cellulose and at least one other additive for ceramic enamel.

The glaze slips thus obtained are applied in raw or baked ceramic bodies, such as artistic ceramics, crockery, tiles, roofing tiles, bricks, heavy clay products and sanitary ware.

ANTECEDENTS OF THE TECHNIQUE Products made of ceramic, more traditional, such as tiles and toilets, are made of a ceramic body that gives shape and mechanical properties to the object; the ceramic body generally has some porosity and poor aesthetic qualities.

The ceramic body, which is defined as "raw" or alternatively "baked", is usually coated with a ceramic layer, called ceramic glaze; the ceramic enamel is sintered by firing, in such a way that adequate superficial aesthetic qualities are obtained and, in the meantime, it becomes a barrier to proof of fluids; in fact, after firing, the ceramic glaze usually has no porosity and is generally resistant to abrasion and attack by chemical agents.

The enamel is applied mainly on the surface of the ceramic body, dispersed / suspended in a suitable vehicle, usually water, or in some special application, dry dusting a dry mixture on the surface of the ceramic body. Traditional liquid ceramic enamels are suspensions of various mineral and metallic powdered oxides, which can be applied by directly submerging the pieces in the enamel, pouring the enamel onto the piece, spraying it on the piece with an airbrush or similar tool, with a brush or any tool that achieves the desired effect.

Liquid ceramic enamels, also called ceramic enamel slips, generally contain, finely dispersed in water, silica to form the glass, also in the form of a frit (precooked vitreous component); mixtures of metal oxides, usually in the form of pretreated natural minerals, such as alkaline earth metal oxides which act as a flux and allow the enamel to melt at a particular temperature; alumina to harden the enamel and prevent it from running off the piece; ceramic pigments, such as oxides or carbonates of transition metals.

Since most of the ingredients cited above are heavy ingredients, and in order to obtain an appropriate coating before and after cooking, it is necessary to add some particular additive to liquid ceramic enamels. These additives, often of an organic nature, are added, alone or as compositions, to the glazes to give them specific properties that are required during the application. They do not participate directly in the vitrification process, but they are able to give special characteristics to the enamel slip, useful for the later application in the ceramic body or to the glass formed for successive treatments.

These additives for ceramic enamel are well known in the art, and additional information can be found in the literature, for example, in Fortuna D., "Sanitaryware", Gruppo Editoriale Faenza Editrice, p. 61-64 (2000) and Stefanov S. and Batscharow S., "Ceramic Glazes", Bauverlag GmbH (1989).

The most common ceramic glaze additives are: suspending agents, such as water-swellable clays; thickening agents, such as carboxymethyl cellulose, alginates, natural gums and acrylic (co) polymers; preservatives, biocides, defoamers, dispersants (fluid izantes), such as (co) acrylic acid polymer of medium / low molecular weight; binders; deflocculants; equalizing agents and plasticizers.

Many of these additives are added to enamel slips as powders. Dusts, by their nature, have very large surface areas, susceptible to moisture and / or bacterial growth.

The handling of such powders and the generation of dust during processing, creates environmental and health problems, which must be addressed by the manufacturer and the consumer.

In addition, the suspending agents and the thickening agents in the form of powders are difficult to dissolve in the enamel slip and if they are not stirred for a sufficient time and / or with a mixer with high shear stress, they can create chunks or aggregates in the enamel slip. After preparation, the enamel slips are screened in order to remove residual impurities and aggregates. If they do not dissolve completely, the traces or aggregates of the additives can considerably increase the time required for screening. In addition, a partial dissolution of the rheology modifier may require a time consuming viscosity correction of the enamel slip or, if left uncorrected, it may cause serious enamel defects in the end products, such as equalization problems, creep or drag, which are well known to those skilled in the art. In addition, the exact dosage and loading of the sprayed additives, which usually have different densities and different particle sizes, are a source of additional difficulties.

A typical solution for these problems commonly used in many fields is to granulate the pulverized compounds or compositions. Unfortunately, the granules obtained during the granulation process are of different shapes and dimensions, thus making It is necessary, to sift the granulated material, in order to select the granules that have the dimensions above a minimum value. In addition, granulation does not remove dust. In fact, a percentage of this powder, even if it is small, remains trapped between the granules and tends to disperse.

It has now been found that the use of the compositions of these additives in the form of extruded pellets can solve all the difficulties mentioned above. The composition and dimensions of the pellets can be easily controlled, in order to avoid risks and optimize the processing, handling / shipping, dosing of the load, etc. At the same time, the extruded pellets are really compact and do not produce dust when handled and have a low dissolution rate, as compared to the powders, which significantly reduce the formation of pieces in the enamel slip.

As far as the Applicant is aware, the use of extruded pellets obtained by extruding a mixture of two or more additives for the ceramic enamel, for the preparation of enamel slips, has not been described in the literature.

By "pellet", we mean any composition with solid form, including, but not limited to, tablets, beads, flakes, briquettes, bars or blocks.

BRIEF DESCRIPTION OF THE INVENTION Therefore, it is a fundamental object of the present invention, the use of exempt pellets comprising: a) from 5 to 85% by weight as dry matter of a carboxymethyl cellulose (CMC), b) from 5 to 85% by weight as dry matter of at least one other additive for ceramic enamel, in which, the sum of a) + b) represents at least 40% by weight of its dry matter, for the preparation of ceramic enamel slips, the pellets are used in an amount comprised between 0.05% and 5% by weight, based on the weight of the ceramic enamel slip.

DETAILED DESCRIPTION OF THE INVENTION Preferably, the extruded pellets of the invention comprise: a) from 20 to 75% by weight as dry matter of a CMC and b) from 20 to 75% by weight as dry matter of at least one other additive for ceramic enamel.

The carboxymethyl cellulose a) suitable for the embodiment of the present invention can be chosen from those commonly used in the field of ceramics, and known to those skilled in the art. The carboxymethyl cellulose preferred for the embodiment of the present invention has a degree of substitution comprised between 0.5 and 1.5, more preferably between 0.6 and 1.2, still more preferably, from 0.7 to 1.1. his Brookfield LVT® viscosity, at 2% by weight (weight) in water, 60 rpm and 20 ° C, is between 5 and 30,000 mPa-s, preferably between 10 and 15,000 mPa > s. The carboxymethyl cellulose useful for the embodiment of the present invention may be technical or purified carboxymethyl cellulose, having a percentage of active substance comprised between 55 and 99.5% by weight, of dry matter, preferably 70 to 98.5, and a water content of about 2-12% by weight.

The ceramic enamel additive b) is preferably selected from the group consisting of suspending agents, thickening agents other than CMC, preservatives, biocides, antifoams, dispersants, binders, deflocculants, leveling agents, plasticizers, purifying agents and mixtures of the same.

The suspending agents improve the stability and flowability of the dispersion and also allow a higher percentage of suspended solids to be incorporated into the dispersion. Suitable suspending agents are clays swellable with water and sodium or magnesium chloride. Water-swellable clays are the preferred suspending agents. With the expression "clays inflatable with water", we mean clays that are capable of adsorbing water.

Examples of these clays are bentonite, montmorillonite, kaolinite, hectorite, attapulgite, smectite and others. The most popular clay is standard bentonite, which may contain a small amount of iron. Another useful clay is hectorite, which is very plastic and free of iron and belongs to the family of smectite minerals. It is sold under several trade names, including Bentone®, Hectabright®, Macaloid® and VeeGum®. Synthetic smectites can also be used for the same purpose.

Suitable thickening agents other than CMC, which have agglomeration, film formation, suspension and water retention properties, are natural water soluble polymers, such as or synthetically derived, such as starch and starch derivatives, guar and guar derivatives. , tamarind and its derivatives, xanthana gum, alginates, gum diutan, gum arabic and tragacanth gum. Cellulose and cellulose derivatives, other than CMC, may also be used, such as hydroxyethyl cellulose, hydroxypropyl cellulose, methyl hydroxypropyl cellulose. Suitable additional thickening agents are synthetic polymers, such as polymer based on high molecular weight acrylic acid or polyvinyl pyrrolidone and their copolymers. Advantageously, mixtures of thickening agents can also be used.

As its name suggests, the dispersant ensures that the solid is dispersed evenly throughout the aqueous medium. Any of the dispersants that are normally used for the aqueous ceramic slurries are useful in the preparation of the pellets of the present invention. Examples of these dispersants are water-soluble salts of low / medium molecular weight acrylic (co) polymers, such as (meth) acrylic acid homopolymers; polyphosphates, for example, tripolyphosphate and hexametaphosphate, humic acids; lignin sulfonates; sodium silicates, sodium carbonate and mixtures thereof. Preferred dispersants are water-soluble salts of low / medium molecular weight acrylic (co) polymers and polyphosphates. Suitable biocides and preservatives are, for example, p-chloro-m-cresol, o-phenyl phenol, 2-bromo-2-nitropropan-1,3-diol (Bronopol) or compounds of the isothiazolin-3 class. derivatives, such as benzisothiazolinone (BIT), 5-chloro-2-methyl-4-isothiazolin-3-one (CIT or CMIT) and 2-methyl-4-isothiazolin-3-one (MIT). Other examples are sodium or zinc pyrithione, parabens, sodium benzoate, formaldehyde releasers, etc. They are used both in the form of powders and liquids, also as synergistic mixtures.

Examples of defoamers and purging agents suitable for the embodiment of the present invention are aluminum stearate, ethylene / propylene oxide copolymers, polydimethyl siloxane, colloidal silica, mineral oils and mixtures thereof.

Examples of ers that can be used in the present invention are polyvinyl alcohol, polyvinyl acetate or partially hydrogenated polyvinyl acetate, polyacrylates or anionic polyacrylamides, polyurethanes, styrene / butadiene resins and mixtures thereof.

Plasticizers are usually added to reduce the elastic modulus of enamel slips and their internal stress during cooking, thus decreasing the likelihood of crack formation. Examples of plasticizers are glycerol, sorbitol, glycols, such as triethylene glycol or propylene glycol, (co) polymers of ethylene oxide / propylene oxide; acids fatty or fatty amides; alkanol amines such as triethanol amine; monoesters of glycerol fatty acid or glycols; esters such as monobutyl or dibutyl phthalate, and mixtures thereof. Preferred plasticizers are polyethylene and / or polypropylene glycols.

Other ingredients that can be advantageously added to the extruded pellets of the invention are fillers, disintegrating agents such as polyvinylpyrrolidone, dextran and starch or a mixture of carboxylic acids, for example, citric or tartaric acid, and water soluble carbonate or bicarbonate, that is, sodium carbonate; plasticizers for extrusion, such as ethyl cellulose and polyethylene glycol.

The method of preparing the extruded pellets comprises the following phases: 1) preparing a hydrated mixture of a) and b); 2) extruding the hydrated mixture to form an extruded material; 3) crush the resulting extruded material to create a formed product (pellets).

By conventional means, the CMC, the water and the ceramic additives are mixed to form a hydrated mixture (phase 1). This can be done in an external mixing device and / or inside the extruder.

The water content of the hydrated mixture is only important in that it should be high enough to allow intimate and uniform mixing of the different components and should allow the extrusion of the mixture. Conversely, the water content of the hydrated mixture does not It must be so high that it does not hold its shape after it extrudes. Generally, the water content of the hydrated mixture is from 5.0 to 50% by weight.

The material in the extruder is heated to, or maintained at a temperature in the range of about 20 to about 100 ° C. The optimum temperature for extrusion will vary somewhat, depending on the components of the mixture, but the optimum temperature can easily be determined empirically. The temperature of the mixture may vary depending on where it is in the extruder, but generally, a uniform temperature profile is preferred. The temperature referred to herein is the temperature of the mixture in the extruder, just before it passes through the die. High temperatures that can cause decomposition should be avoided.

The hydrated mixture is extruded through a die, preferably a die with multiple orifices. In general, the shape and size of the holes fix the shape and size of the cross section of the extrudate. Although any form of hole, i.e., circle, triangle, square or rectangle can be used, it is preferred that the extrusion of the hydrated mixture be through equiaxed holes. Equiaxial orifices are holes that have approximately equal dimensions in all directions. The cross-sectional area of the holes should be sufficiently small, so that the fibers of the hydrated extruded mixture are aligned parallel to each other, in formed filaments closely (strands). On the other hand, the cross-sectional area of the hole should not be so small that an excessive amount of energy must be exerted to press the hydrated mixture through the holes. Generally, the holes are of dimensions ranging from 1.0 to 6.0 mm, preferably from 2.0 to 3.5 mm.

The extrusion can be done with any device that applies sufficient pressure to push the hydrated mixture through the extrusion orifices, at a temperature that keeps the mixture hydrated. For example, a pump type extruder, such as a positive displacement piston or a gear pump may be used. Another example of suitable extrusion equipment is a screw type extruder, which advances the hydrated mixture by means of a screw rotating inside the cylinder. A twin screw extruder in a parallel or counter rotating, intergranular or non-intergranular rotation mode can be used in the processes of the invention, but likewise, a single screw extruder or an extruder with multiple screws can also be suitable, provided the condition that the mixing is achieved. Screw type extruders are not as energy efficient as pump type extruders and convert much of the energy into heat. This causes the temperature of the mixture to increase and dehydration to occur. Thus, when a screw type extruder is used, it is generally necessary to use a cooling device to keep the mixture hydrated at a temperature below 100 ° C.

Usually, the extrusion process is carried out at pressures well above atmospheric pressure, preferably, the extrusion is carried out at pressures of about 20 to about 160 bars.

The extruded material is a firm material that perishes uniform in texture and color. Generally, the extruded material is in the form of long, narrow filaments. The filaments have a uniform cross-sectional area that is approximately the same as the extrusion holes described above. The extruded material has a residual moisture content ranging from 5.0 to 50% by weight, preferably from 15 to 30% by weight.

In order to reduce the filaments in pellets, it is necessary to grind the extrudate (phase 3).

Grinding can be accomplished using standard equipment known in the art. Typical crushing devices are air-swept impact mills, ball mills, hammer mills and disk mills. This is preferably done in an air-swept impact mill, because other mills, ie, ball mills, have the tendency to over-crush the product into fine particles that are pulverulent. In addition, an air sweeping impact mill will dry the extruded material, if necessary, by blowing hot air through the mill.

Another method for grinding the extruded material is to cut it with a die-face cutter. A die-cutter cutter operates by moving a blade through the stationary die or moving a die through the stationary blade. Thus, the ceramic additive is cut as it is extruded through the plurality of holes in the die.

The size of the extrusion hole sets two of the dimensions of the product. Therefore, it is only necessary to cut the filaments to shorten the length. Typically, the extruded material is cut at a length / diameter ratio of 0.5 to 3, preferably at a length / diameter ratio of 1 to 2.

It may be advantageous to dry the extruded pellets. The drying of the extruded material can be accomplished with standard drying equipment and with methods known in the art. Typical dryers include belt dryers and fluid bed dryers. The dried extruded pellets have a residual moisture content that generally ranges from 5.0 to 15% by weight.

In a preferred embodiment, the ceramic enamel slips contain 0.2 to 3% by weight of the extruded pellets of the invention.

All the enamels normally used in the ceramic industries and well known to those skilled in the art can be prepared using the extruded pellets of the invention. Several examples of formulations for ceramic enamel can be found in the literature, such as: Fortuna D., "Sanitaryware", Gruppo Editoriale Faenza Editrice, (2000) and Stefanov S. and Batscharow S., "Ceramic Glazes", Bauverlag GmbH ( 1989).

As already mentioned, the typical components of ceramic glazes are silica, fluxes, alumina and ceramic pigments.

Silica and alumina can be added to enamels by the addition of minerals, such as: quartz, flint, clay granules, kaolin, feldspar or mixtures thereof. Silica can also be added to the enamel in the form of frits, the term fried refers to the granulated or particulate material obtained when the molten glass is poured in cold water. Frits are usually mixtures of various mineral materials, which contain, among others, silica, alumina, metal oxides, boron oxide.

The fluxes lower the melting point of the glass formers. Non-exhaustive examples of fluxes are alkali and alkaline earth oxides and carbonates.

The ceramic pigments useful in the ceramic glaze of the invention are solid sinterable materials. Examples of suitable ceramic pigments include iron, titanium, copper, chromium, zinc, magnesium, aluminum, cobalt and oxides or cadmium salts, and silicates of zirconium and praseodymium.

The extruded pellets of the invention can be added to the enamel in the mill during the grinding or during the preparation of the enamel slip, such as or as a dispersion in water at a concentration ranging from 1 to 30% by weight; they are preferably added to the components of the ceramic enamel slip in dry form.

For liquid applications, the enamels are crushed and sieved normally, then suspended in a vehicle such as water, obtaining the enamel slip. The ratio between the solid materials and the vehicle is between 85/15 and 40/60 by weight. Often, the grinding of the enamels is done directly in the presence of the vehicle, to provide the enamel slip in a single operation.

The pellets exempted from the invention can also be used for the preparation of engobes, which are a particular class of enamels. A slip is an opaque coating that is frequently applied to the ceramic body before enameling. Its function is to mask the ceramic body, for example, when it is produced using red clay. Slips conventionally contain frits and raw materials, but the content of the frit is typically much less than in a normal enamel.

The enamel slip of the present invention can be applied to raw or baked ceramic bodies, such as artistic ceramics, crockery, tiles, roofing tiles, bricks, heavy clay products and sanitary ware, using any of the conventional application techniques known from the art. those with experience in the technique. Application techniques such as disk and bell applications, immersion, spraying, screen printing, brush application and electrostatics can be used.

The enamel slip of the invention is stable with storage for several days without changing its rheological profile and can used as if it had been prepared recently.

EXAMPLES EXAMPLES 1-3 The solid ingredients of Table 1 were homogenized in a mixer, using a "K" shaped stirrer. During the homogenization, demineralized water was added slowly (in approximately 10 minutes) to the mixture, avoiding agglomeration of the material.

TABLE 1 * active at 74% in the dry matter; DS 0.72; moisture 24% by weight; Brookfield® LVT viscosity (6% solution as dry matter, 60 rpm, 20 ° C) 300 mPa-second.

The blends of Examples 1-3 were transferred to a Bausano extruder equipped with 2 counter-rotating screws, a multi-hole 2.5 mm die and a die face cutter.

The speed of the screws and the cutter was adjusted to produce approximately 50-80 g / minute of granules of approximately 2.5 mm wide and 2.6 mm long. The internal temperature and the pressure during the extrusion were around 60-70 ° C and 130 bars, respectively.

The extruded pellets were dried in a fluid bed at 80 ° C, to obtain a residual moisture of about 7% by weight.

Table 2 shows the results of the dissolution test of 30 g of each mixture in 300 ml of demineralized water, under constant agitation with a magnetic bar stirrer.

The results are reported as the time required to reach the maximum Brookfield LVT viscosity, measured at 25 ° C and 60 rpm.

TABLE 2 The stability of the extruded pellets of Examples 1-3 to the mechanical stress was evaluated by stirring the pellets for 30 minutes on a tared stainless steel screen (80 mesh), in the presence of a hard sphere (2 cm or.d.) of silica.

At the end of the test, the amount of dust that passes through the 80 mesh screen was determined. For each sample, the amount of powder was below 0.1%.

Application test The extruded pellets of Example 2 were compared with the same composition of Example 4 (see Table 3), prepared simply by physically mixing the different ingredients.

TABLE 3 * active at 74% in dry matter; DS 0.72; humidity 6% by weight; Brookfieid® viscosity LVT (6% solution as dry matter, 60 rpm, 20 ° C) 300 mPa-second.

The rate of dissolution in an enamel slip of the two ceramic additives was evaluated.

Two enamel tile slips were prepared, transferring in two bottles of 1000 ml, the amount in g of the ingredients reported in Table 4.

TABLE 4 * Comparative Both enamel slips were crushed in a mill with vibration for 15 minutes and then poured into a beaker. precipitates of glass of 1000 ml.

The main parameters (Brookfield RVT viscosity, Viscosity with the Ford Cup, Density and% of Residues) of the glaze slips thus obtained were measured at 25 ° C.

The% residue was determined by sieving the two enamel slips with an ASTM sieve of 150 microns, tared (100 mesh) and determining the difference in weight after drying in an oven at 105 ° C for 2 hours.

The results are reported in Table 5.

The results of the tests of the behavior of the solution show that the extruded pellets of the invention have a dissolution behavior comparable to that of a rheology modifier of the known art.

TABLE 5 * Comparative Due to their physical characteristics, the extruded pellets of the invention avoid the production of volatile dust when handled and allow simpler procedures for the preparation of the enamel slip, together with the simplest and most accurate dosage of the additives.

Claims

NOVELTY OF THE INVENTION CLAIMS 1. - The use of extruded pellets, comprising a) from 5 to 85% by weight as dry matter of a carboxymethyl cellulose (CMC), b) from 5 to 85% by weight as dry matter of at least one other additive for ceramic enamel, in which the sum of a) + b) represents at least 40% by weight of its dry matter, for the preparation of ceramic enamel slips, the pellets are used in an amount between 0.05% and 5% by weight, based on in the weight of the ceramic enamel slip. 2. - The use as claimed in claim 1, wherein the extruded pellets comprise: a) from 20 to 75% by weight as dry matter of a carboxymethyl cellulose; b) from 20 to 75% by weight as dry matter of at least one other additive for ceramic enamel. 3. - The use as claimed in claim 1, wherein the carboxymethyl cellulose a) has a degree of substitution comprised between 0.5 and 1.5 and a Brookfield LVT® viscosity, at 2% by weight in water, 60 rpm and 20 ° C, from 5 to 30,000 mPa-s. 4. - The use as claimed in claim 3, wherein the carboxymethyl cellulose a) has a degree of substitution comprised between 0.6 and 1.2 and a Brookfield LVT® viscosity, at 2% by weight in water, 60 rpm and 20 ° C, from 10 to 15,000 mPa-s. 5. - The use as claimed in claim 1, wherein the additives for ceramics b) are chosen from the group consisting of suspending agents, thickening agents other than CMC, preservatives, biocides, antifoams, dispersants, binders, deflocculants, leveling agents , plasticizers, purging agents and mixtures thereof. 6. - The use as claimed in claim 5, wherein the suspending agents are water-swellable clays, chosen from among bentonite, montmorillonite, kaolinite, hectorite, attapulgite and smectite and mixtures thereof. 7. - The use as claimed in claim 5, wherein the thickening agents other than CMC are chosen from natural water-soluble polymers, such as derivatives, cellulose derivatives other than CMC, synthetic polymers and mixtures thereof. 8. - The use as claimed in claim 5, wherein the dispersants are chosen from water-soluble salts of low / medium molecular weight acrylic (co) polymers, polyphosphates, humic acids, lignin sulphonates, sodium silicates, carbonate sodium and mixtures thereof. 9. - The use as claimed in claim 5, wherein the biocides are chosen from isothiazolin-3-one derivatives, o-phenyl phenol derivatives, p-chloro-m-cresol, pyrithione salts, parabens, formaldehyde releasers and mixtures thereof. 10 -. 10 - The use as claimed in claim 5, wherein the defoamers and / or purging agents are chosen from aluminum stearate, copolymers of ethylene / propylene oxide, polydimethyl siloxane, colloidal silica, mineral oils and mixtures thereof.

1. The use as claimed in claim 5, wherein the binders are chosen from polyvinyl alcohols, polyvinyl acetate or partially hydrolyzed polyvinyl acetate, polyacrylates or anionic polyacrylamides, polyurethanes, styrene / butadiene resins and mixtures thereof. same. 12 -. 12 - The use as claimed in claim 5, wherein the plasticizers are chosen from glycerol; sorbitol; glycols, (co) ethylene oxide / propylene oxide co-polymer; fatty acids of fatty amides; alkanol amines, fatty acid monoesters of glycerol or glycols, mono or diesters of italic acid and mixtures thereof.